US4514357A - Production of molded articles having excellent optical characteristics - Google Patents

Production of molded articles having excellent optical characteristics Download PDF

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Publication number
US4514357A
US4514357A US06/450,039 US45003982A US4514357A US 4514357 A US4514357 A US 4514357A US 45003982 A US45003982 A US 45003982A US 4514357 A US4514357 A US 4514357A
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US
United States
Prior art keywords
resin
phosphite
average molecular
molecular weight
polycarbonate
Prior art date
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Expired - Lifetime
Application number
US06/450,039
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English (en)
Inventor
Yoshikazu Kawaguchi
Seiichro Maruyama
Hiroyuki Kawasaki
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Mitsubishi Chemical Corp
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Mitsubishi Chemical Industries Ltd
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Assigned to MITSUBISHI CHEMICAL INDUSTRIES LIMITED reassignment MITSUBISHI CHEMICAL INDUSTRIES LIMITED ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: KAWAGUCHI, YOSHIKAZU, KAWASAKI, HIROYUKI, MARUYAMA, SEIICHRO
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Publication of US4514357A publication Critical patent/US4514357A/en
Assigned to MITSUBISHI KASEI CORPORATION reassignment MITSUBISHI KASEI CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: MITSUBISHI CHEMICAL INDUSTRIES LIMITED
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Classifications

    • GPHYSICS
    • G11INFORMATION STORAGE
    • G11BINFORMATION STORAGE BASED ON RELATIVE MOVEMENT BETWEEN RECORD CARRIER AND TRANSDUCER
    • G11B7/00Recording or reproducing by optical means, e.g. recording using a thermal beam of optical radiation by modifying optical properties or the physical structure, reproducing using an optical beam at lower power by sensing optical properties; Record carriers therefor
    • G11B7/24Record carriers characterised by shape, structure or physical properties, or by the selection of the material
    • G11B7/26Apparatus or processes specially adapted for the manufacture of record carriers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • C08K5/51Phosphorus bound to oxygen
    • C08K5/52Phosphorus bound to oxygen only
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • C08K5/51Phosphorus bound to oxygen
    • C08K5/52Phosphorus bound to oxygen only
    • C08K5/524Esters of phosphorous acids, e.g. of H3PO3

Definitions

  • This invention relates to molded articles having excellent optical characteristics. More particularly, it relates to molded articles having excellent transparency and a reduced degree of optical strain and also to a method for producing such molded articles.
  • Molded articles used for optical purposes in the form of, for example, plates, sheets, boxes, blocks or other various shapes should not only be transparent, but also have a reduced degree of optical strain.
  • digital signal recording discs such as digital audio discs, digital video discs and signal recording discs for electronic computers should have excellent transparency and small optical strain.
  • the retardation is needed to be not more than 60 m ⁇ , preferably not more than 40 m ⁇ .
  • the warpage should be so small that for the digital audio disc, it is needed to be not more than 0.2 mm, preferably not more than 0.1 mm.
  • the good flow of the resin melt may be attained by a method in which the injection molding is effected at high resin temperatures.
  • high resin temperatures are disadvantageous in that the resin may be colored or yellowed such as by decomposition of the resin, impeding the transparency of the resultant molding.
  • polycarbonate resins having low molecular weights may be used.
  • such polycarbonate resins e.g. polycarbonate resins having an average molecular weight less than 12000, considerably lower in molecular weight when injection molded, leading to the disadvantage in that their mechanical properties greatly lower and the resultant molding will break upon release of the molding.
  • the above object can be achieved by a molded article or molding obtained by injection molding at a resin temperature of 330°-400° C. and at a mold temperature of 50°-110° C. a resin composition of a bis(hydroxyphenyl)alkane polycarbonate resin having an average molecular weight of 12000 to 18000 and containing 0.005 to 0.5 wt %, based on the resin, of a phosphorous ester represented by the general formula ##STR2## wherein R 1 and R 2 independently represent an alkyl or aryl group, and R 3 represents hydrogen, an alkyl, or aryl group.
  • the bis(hydroxyphenyl)alkane polycarbonate resins used in the present invention are those which have an average molecular weight of 12000 to 18000 and are obtained by reacting bis(hydroxyphenyl)alkanes and a carbonate such as phosgene or diphenyl carbonate.
  • the average molecular weight is calculated from ⁇ sp, which was measured at 20° C. using a methylene chloride solution of 6.0 g/l of the polycarbonate resin, according to the following formulae
  • C represents a concentration of the polycarbonate resin (g/l)
  • [ ⁇ ] is an intrinsic viscosity
  • K' is a constant of 0.28
  • K is a constant of 1.23 ⁇ 10 -5
  • M is an average molecular weight
  • is a value of 0.83.
  • the average molecular weight is usually controlled by adding a short stopper such as phenol, p-tertiary butylphenol or the like at the production of the polycarbonate resin.
  • bis(hydroxyaryl)alkanes examples include bis(4-hydroxyphenyl)methane, 1,1-bis(4-hydroxyphenyl)ethane, 2,2-bis(4-hydroxyphenyl)propane, 2,2-bis(4-hydroxyphenyl)butane, 2,2-bis(hydroxyphenyl)octane and the like. Additionally, within a range not impeding the physical properties of the resulting molded articles such as discs, other compounds may be used in admixture with the above-mentioned alkanes.
  • These other compounds include, for example, bis(hydroxyaryl)cycloalkanes such as 1,1-bis(4-hydroxyphenyl)cyclohexane, dihydroxydiphenyl ethers such as 4,4'-dihydroxydiphenyl ether, dihydroxydiphenylsulfides such as 4,4'-dihydroxydiphenylsulfide, dihydroxydiphenylsulfoxides such as 4,4'-dihydroxydiphenylsulfoxide, dihydroxydiphenylsulfones such as 4,4'-dihydroxydiphenylsulfone, and the like.
  • dicarbonate resins a polycarbonate resin which is prepared from 2,2-bis(4-hydroxyphenyl)propane(bisphenol A) is preferred.
  • the polycarbonate resins should have an average molecular weight of 12,000 to 18,000, preferably 13,000 to 17,500. Too high average molecular weights are disadvantageous in that in order to make molded articles having a reduced degree of optical strain, the molding has to be effected at a resin temperature exceeding 400° C., involving decomposition of the resin at such high temperatures.
  • the resulting molded articles will have silver streaks on the surface thereof or undergo coloration.
  • too low average molecular weights make it possible to suppress the optical strain to a substantial extent, but the molecular weight of the resin lowers so considerably at the time of the molding that the physical properties of the resin deteriorate and thus the resulting molding tends to break upon release from a mold. Even though moldings are obtained, their mechanical strengths are unfavorably low.
  • the phosphorous esters used in the practice of this invention are diesters or triesters obtained from phosphorous acid and alcohols or phenols.
  • examples of R 1 and R 2 are respectively, an alkyl group such as butyl, hexyl, octyl, 2-ethylhexyl, nonyl, decyl, dodecyl, octadecyl, pentaerythrityl, cyclohexyl and the like, and an aryl group such as phenyl, tolyl, nonylphenyl and the like.
  • R 3 represents hydrogen, or the above-mentioned alkyl or aryl groups.
  • Examples of the phosphorous esters include tributyl phosphite, tris(2-ethylhexyl)phosphite, tridecyl phosphite, tristearyl phosphite, triphenyl phosphite, tricresyl phosphite, tris(nonylphenyl) phosphite, 2-ethylhexyldiphenyl phosphite, decyldiphenyl phosphite, phenyldi-2-ethylhexyl phosphite, phenyldidecyl phosphite, tricyclohexyl phosphite, distearylpentaerythrityl diphosphite, diphenylpentaerythrityl disphosphite, and the like.
  • the amount of the phosphorous esters is in the range of 0.005 to 0.5 wt %, preferably about 0.01 to 0.2 wt %, of the polycarbonate resin. Too small amounts of the phosphorous ester lead to the disadvantage that the coloration and deterioration in transparency caused by decomposition of the resin cannot be suppressed. On the contrary, too large amounts lead to decomposition of phosphorous esters themselves, causing silver streaks to be formed on the surface of molded articles.
  • the phosphorous ester can be incorporated in a polycarbonate resin by a variety of methods as usually employed for preparation of ordinary resin compositions.
  • the methods include a dry blending of both ingredients, a melt mixing of the blend using an extruded, etc., and a method in which master pellets containing a larger amount of phosphorous esters are first prepared and then admixed with polycarbonate resin pellets.
  • the polycarbonate resin containing a phosphorous ester in such a manner as mentioned above is injection molded at a resin temperature of 330° to 400° C. and at a mold temperature of 50° to 110° C.
  • too high resin temperatures should be avoided because the resin decomposes, so that coloration and silver streaks take place, resulting in poor transparency.
  • too low resin temperatures are disadvantageous in that the polycarbonate resin used in the present invention does not show satisfactory melt flowability and thus moldings of low optical strains cannot be obtained.
  • Preferable resin temperatures are approximately in the range of 335° to 390° C.
  • the mold temperature is generally in the range of 50° to 110° C., preferably 60° to 105° C. Higher mold temperatures are unfavorable since great deformation takes place at the time of release of the resulting molding and thus there cannot be obtained moldings having a small degree of warpage. Lower temperatures result in optically strained moldings.
  • the injection rate is not less than 70 ml/sec, preferably 80 to 300 ml/sec.
  • the injection rate is meant a rate of charging a melt into a mold. This rate is indicated herein by an amount of a melt per unit time during the course of from the start of the injection till a stage of dwelling. This amount is calculated from the product of the forward speed of a screw of an injection machine and the inner sectional area of the cylinder.
  • Molded discs having a thickness of 1.2 mm and a diameter of 120 mm were measured at the central portion thereof by means of a polarizing microscope made by Carl Zeiss Co., Ltd. and attached with a calcite compensator and the retardation was indicated by m ⁇ .
  • Discs of the same size as mentioned above were each placed on a flat plate and a height at the most warped end portion from the plate was measured by means of a coordinate measuring machine made by Mitsutoyo Co., Ltd. and indicated by mm.
  • a 3.5 ounce injection molding machine (IS 75S, made by Toshiba Machine Co., Ltd.) was used to give a 3.2 mm thick and 50 mm ⁇ test piece under conditions of a resin temperature of 355° C. and a mold temperature of 80° C.
  • the transmittance was measured according to the method prescribed in ASTM D 1003 using Haze Meter TC-5D made by Tokyo Denshoku Co., Ltd. and indicated by %.
  • a 3.5 ounce injection molding machine of the same type as used above and a 2 mm thick mold for measurement of spiral flow were used to conduct the injection molding under conditions of a resin temperature of 355° C., a mold temperature of 80° C. and an injection pressure of 850 kg/cm 2 , and the flow length was indicated by mm.
  • This polycarbonate resin was admixed with 0.05% of tridecyl phosphite, 2-ethylhexyldiphenyl phosphite and tris(nonylphenyl)phosphite.
  • the respective resin compositions had total light transmittances of 91%, 90% and 87%, and melt flowabilities of 550 mm, 540 mm and 540 mm.
  • the phosphite-free resin had a total light transmittance of 81% and a melt flowability of 530 mm.
  • Preparatory Example A was repeated except that 0.347 part of p-tertiary butylphenol was used, thereby obtained a polycarbonate resin having an average molecular weight of 15500.
  • This polycarbonate resin was admixed with tridecyl phosphite in an amount of 0.02% and 0.15% and the resulting resin compositions had both a total light transmittance of 91% with melt flowabilities being 850 mm and 900 mm, respectively.
  • a resin composition admixed with 0.02% of tris(nonylphenyl) phosphite had a total light transmittance of 90% and a melt flowability of 820 mm.
  • Preparatory Example A was repeated except that 0.237 part of p-tertiary butylphenol was used, thereby obtained a polycarbonate resin having an average molecular weight of 21800.
  • This polycarbonate resin was admixed with 0.05% of tridecyl phosphite and the resulting resin composition had a total light transmittance of 90% and a melt flowability of 340 mm.
  • the polycarbonate resin flakes with an average molecular weight of 17800 and prepared in Preparatory Example A were admixed with phosphorous esters indicated in Table 1 and charged into a 40 mm ⁇ extruder where they were molten and kneaded at 270° C. and extruded to give pellets.
  • phosphorous ester-containing polycarbonate pellets having average molecular weights indicated in Table 1 were obtained.
  • the respective types of the pellets were charged into a 4 ounce injection molding machine (J 150S, made by Japan Steel Works, Ltd.) and molded into digital audio discs having 1.2 mm thick and 120 mm diameter at respective resin temperatures, mold temperatures and injection rate indicated in Table 1.
  • the resulting discs had retardations and warpages indicated in Table 1.
  • the polycarbonate resin having an average molecular weight of 15500 and prepared in Preparatory Example B were admixed with tridecyl phosphite or tris(nonylphenyl)phosphite in amounts indicated in Table 2, followed by repeating the procedure of Example 1 to obtain digital audio discs.

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  • Chemical & Material Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Manufacturing & Machinery (AREA)
  • Engineering & Computer Science (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Optical Record Carriers And Manufacture Thereof (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Polyesters Or Polycarbonates (AREA)
US06/450,039 1982-01-22 1982-12-15 Production of molded articles having excellent optical characteristics Expired - Lifetime US4514357A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP57008315A JPS58126119A (ja) 1982-01-22 1982-01-22 光学的特性のすぐれた成形物の製造法
JP57-8315 1982-01-22

Publications (1)

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US4514357A true US4514357A (en) 1985-04-30

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US (1) US4514357A (enrdf_load_stackoverflow)
JP (1) JPS58126119A (enrdf_load_stackoverflow)
DE (1) DE3301963A1 (enrdf_load_stackoverflow)
FR (1) FR2520370B1 (enrdf_load_stackoverflow)
GB (1) GB2114501B (enrdf_load_stackoverflow)
IT (1) IT1163020B (enrdf_load_stackoverflow)
NL (1) NL192061C (enrdf_load_stackoverflow)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4762873A (en) * 1985-06-14 1988-08-09 Teijin Chemicals, Ltd. Polycarbonate resin composition
US4764331A (en) * 1984-01-26 1988-08-16 Daicel Chemical Industries, Ltd. Large diameter optical disk substrate made of polycarbonate
US4892692A (en) * 1987-01-30 1990-01-09 Canon Kabushiki Kaisha Process for producing substrate for optical disk by annealing substrate with gradient double refraction distribution
US4980105A (en) * 1989-08-28 1990-12-25 General Electric Company Method for extruder devolatilization of spiro(bis)indane polycarbonates
US5102608A (en) * 1990-01-03 1992-04-07 Stamicarbon B.V. Method for the manufacture of objects from polycarbonate
US5455324A (en) * 1992-08-26 1995-10-03 Mitsubishi Chemical Corporation Aromatic polycarbonate resin of improved color
US5464930A (en) * 1986-10-10 1995-11-07 General Electric Company Article for use in optical application formed from linear polycarbonate resins
US5519106A (en) * 1992-08-26 1996-05-21 Mitsubishi Chemical Corporation Process for the preparation of aromatic polycarbonate resins
USRE35499E (en) * 1988-11-16 1997-04-29 The Dow Chemical Company Elimination of monocarbonate from polycarbonate
EP0794209B1 (en) * 1996-03-07 2003-05-28 Idemitsu Petrochemical Co., Ltd. End group modified polycarbonates for digital video discs

Families Citing this family (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0723921B2 (ja) * 1982-01-22 1995-03-15 三菱化学株式会社 光学ディスク基板
JPS58180553A (ja) * 1982-04-19 1983-10-22 Idemitsu Petrochem Co Ltd 光学機器用成形素材
JPS60166321A (ja) * 1984-02-10 1985-08-29 Idemitsu Kosan Co Ltd 光学機器用素材
JPH0725871B2 (ja) * 1984-03-28 1995-03-22 三菱瓦斯化学株式会社 ポリカーボネート樹脂光学成形品
JPS60215022A (ja) * 1984-04-10 1985-10-28 Mitsubishi Gas Chem Co Inc ポリカ−ボネ−ト樹脂の製法及びそれを用いた光学成形品
JPS60215020A (ja) * 1984-04-10 1985-10-28 Mitsubishi Gas Chem Co Inc ポリカ−ボネ−ト樹脂光学成形品
JPS6264860A (ja) * 1985-09-17 1987-03-23 Teijin Chem Ltd 光学用成形材料
JPH0620783B2 (ja) * 1986-01-31 1994-03-23 三菱化成株式会社 ポリカ−ボネ−ト樹脂製光デイスク基板の製造法
JPH0620784B2 (ja) * 1986-03-26 1994-03-23 三菱化成株式会社 ポリカ−ボネ−ト樹脂よりなる光デイスク基板の製造法
GB2188862B (en) * 1986-04-12 1989-12-28 Duncan Barton Miller A method for the manufacture of cylindrical sound records
JPH0618890B2 (ja) * 1986-06-23 1994-03-16 三菱化成株式会社 ポリカ−ポネ−ト成形材料
JPH0774303B2 (ja) * 1988-04-27 1995-08-09 出光石油化学株式会社 ポリカーボネート組成物及びその製造方法
JP2804596B2 (ja) * 1990-04-19 1998-09-30 ダイセル化学工業株式会社 ポリカーボネートの製造法
JPH0415221A (ja) * 1990-05-08 1992-01-20 Daicel Chem Ind Ltd ポリカーボネートの製造法
US5203671A (en) * 1991-07-09 1993-04-20 C&D Robotics Apparatus for palletizing bundles of paper
JP2836680B2 (ja) * 1996-12-26 1998-12-14 三菱化学株式会社 ポリカーボネート樹脂よりなる光ディスク基板の製造法
JP2002069219A (ja) * 2000-08-31 2002-03-08 Teijin Chem Ltd ポリカーボネート樹脂組成物成形体

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3305520A (en) * 1965-04-06 1967-02-21 Bayer Ag Polycarbonates stabilized by phosphites
US3763063A (en) * 1972-06-14 1973-10-02 Gen Electric Color stabilized polycarbonate composition containing a cadmium or cerium salt of an alkanoic acid an alkanoic acid and an organic phosphite
JPS5120259A (ja) * 1974-07-26 1976-02-18 Dainippon Printing Co Ltd Purasuchitsukurenzunoseizoho
US4008031A (en) * 1975-08-22 1977-02-15 Weber Hermann P Apparatus for injection molding lenses
US4076686A (en) * 1973-01-23 1978-02-28 General Electric Company Heat stabilized polycarbonate resin
US4197384A (en) * 1977-12-28 1980-04-08 General Electric Company Stabilized polycarbonate compositions
US4254065A (en) * 1979-04-04 1981-03-03 Ratkowski Donald J Injection molding of contact lenses
US4276233A (en) * 1978-11-02 1981-06-30 General Electric Company Hindered phenol phosphites
US4284591A (en) * 1980-04-28 1981-08-18 Neefe Optica Lab Inc. Injection molding of optical lenses and optical molds
US4364878A (en) * 1978-08-10 1982-12-21 Omnitech Inc. Method for molding ophthalmic lenses

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1274274B (de) * 1963-04-11 1968-08-01 Bayer Ag Verfahren zur Herstellung von Faeden oder Filmen durch Verformen von hochmolekularenlinearen Polycarbonaten
JPS558189A (en) * 1978-07-05 1980-01-21 Matsushita Electric Ind Co Ltd Television picture receiver
JPS5935360B2 (ja) * 1978-07-21 1984-08-28 プロセス資材株式会社 記録材料
NL7908053A (nl) * 1978-11-02 1980-05-07 Gen Electric Fosfierverbinding, alsmede gestabiliseerd thermo- plastisch materiaal.

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3305520A (en) * 1965-04-06 1967-02-21 Bayer Ag Polycarbonates stabilized by phosphites
US3763063A (en) * 1972-06-14 1973-10-02 Gen Electric Color stabilized polycarbonate composition containing a cadmium or cerium salt of an alkanoic acid an alkanoic acid and an organic phosphite
US4076686A (en) * 1973-01-23 1978-02-28 General Electric Company Heat stabilized polycarbonate resin
JPS5120259A (ja) * 1974-07-26 1976-02-18 Dainippon Printing Co Ltd Purasuchitsukurenzunoseizoho
US4008031A (en) * 1975-08-22 1977-02-15 Weber Hermann P Apparatus for injection molding lenses
US4197384A (en) * 1977-12-28 1980-04-08 General Electric Company Stabilized polycarbonate compositions
US4364878A (en) * 1978-08-10 1982-12-21 Omnitech Inc. Method for molding ophthalmic lenses
US4276233A (en) * 1978-11-02 1981-06-30 General Electric Company Hindered phenol phosphites
US4254065A (en) * 1979-04-04 1981-03-03 Ratkowski Donald J Injection molding of contact lenses
US4284591A (en) * 1980-04-28 1981-08-18 Neefe Optica Lab Inc. Injection molding of optical lenses and optical molds

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4764331A (en) * 1984-01-26 1988-08-16 Daicel Chemical Industries, Ltd. Large diameter optical disk substrate made of polycarbonate
US4762873A (en) * 1985-06-14 1988-08-09 Teijin Chemicals, Ltd. Polycarbonate resin composition
US5464930A (en) * 1986-10-10 1995-11-07 General Electric Company Article for use in optical application formed from linear polycarbonate resins
US4892692A (en) * 1987-01-30 1990-01-09 Canon Kabushiki Kaisha Process for producing substrate for optical disk by annealing substrate with gradient double refraction distribution
USRE35499E (en) * 1988-11-16 1997-04-29 The Dow Chemical Company Elimination of monocarbonate from polycarbonate
US4980105A (en) * 1989-08-28 1990-12-25 General Electric Company Method for extruder devolatilization of spiro(bis)indane polycarbonates
US5102608A (en) * 1990-01-03 1992-04-07 Stamicarbon B.V. Method for the manufacture of objects from polycarbonate
US5455324A (en) * 1992-08-26 1995-10-03 Mitsubishi Chemical Corporation Aromatic polycarbonate resin of improved color
US5519106A (en) * 1992-08-26 1996-05-21 Mitsubishi Chemical Corporation Process for the preparation of aromatic polycarbonate resins
EP0794209B1 (en) * 1996-03-07 2003-05-28 Idemitsu Petrochemical Co., Ltd. End group modified polycarbonates for digital video discs

Also Published As

Publication number Publication date
IT1163020B (it) 1987-04-08
JPS6356043B2 (enrdf_load_stackoverflow) 1988-11-07
GB2114501A (en) 1983-08-24
NL8300013A (nl) 1983-08-16
NL192061B (nl) 1996-09-02
FR2520370B1 (fr) 1986-11-07
GB2114501B (en) 1985-06-26
IT8319113A0 (it) 1983-01-14
DE3301963A1 (de) 1983-08-04
JPS58126119A (ja) 1983-07-27
DE3301963C2 (enrdf_load_stackoverflow) 1990-05-17
FR2520370A1 (fr) 1983-07-29
NL192061C (nl) 1997-01-07

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